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Presented by: Mohamed Hamda
M.A.Sc Candidate
Supervisor: Dr. M. Hamed
On The Effect of Initial Surface
Condition on Pool Boiling of
Nanofluids
Outline
• Pool Boiling.
• Nanofluids.
• Literature review.
• Recent Research in TPL.
• Current research.
• Conclusion.
• Future work.
• Publications.
2
Why Pool Boiling?
• Free Convection - Water: 20 - 100 (W/(m2K))
• Forced Convection - Water: 50 - 10.000
(W/(m2K))
• Boiling Water : 3.000 - 100.000 (W/(m2K))
Boiling Heat transfer coefficients are the highest
among different heat convection mechanisms.
6
Pool Boiling Curve
7
* Heat and Mass Transfer: Fundamentals & Applications,Fourth Edition, Yunus A. Cengel
Thermal conductivity of different
materials
Liquids Metals
k - W/(m.K)
Steel, Carbon 1% 43
Aluminium 205
Copper 401
k - W/(m.K)
Alcohol 0.17
Engine Oil 0.15
Water 0.58
8
• The thermal conductivity of liquids is three orders of
magnitude less than of metals.
• The idea is to increase the thermal conductivity of liquids.
How can we do that?
• Powder of metal has particles of certain size
(10 ~ 100 nm) dispersed into liquid.
• This mixture is now called Nanofluid or
Nanoparticles suspension.
9
Is Nanofluid a novel idea?
• Maxwell model (1881)
– Effective thermal conductivity increases with the
volume fraction of the solid particles as well as the
ratio of the surface area to volume of the particle.
– Confined to millimeter-sized particles.
– Not practical (severe clogging problems).
• Lee, Choi and et al. (1999)
– Reported 20% increase in the thermal conductivity of
CuO nanoparticles (10 nm) suspended in ethylene
glycol.
10
Literature Review
11
* O. Ahmed, M.S. Hamed, Experimental investigation of the effect of particle
deposition on pool boiling of nanofluids
Recent Research in TPL
12
Researcher
(Year)
Experiment
Type
Ra (nm)
Concentration
%
Nanofluid
Material
Particle
size
pH Remarks
Osama
Ahmed
(2011)
Pool Boiling
100 ~
150
50
0.01
0.1
0.5
Al2O3
40 ~ 50
nm
5 and
6.5
Enhancement
&
deterioration
Ahmed
Abd El-
hady
(2013)
Pool and Jet
Impingement
Boiling
20, 80
and 420
0.005
0.01
Al2O3
CuO
10 nm
50 nm
6.5
Enhancement
&
deterioration
Findings from Literature Review
13
• Contradicting results!
• Heat transfer deterioration is always noticed with
nanoparticles deposition on heated surface.
• Most enhancement results were reported for
heated wires.
• Deterioration is more likely to happen with flat or
horizontal heated surfaces.
• Heater geometry affects Nano fluid heat transfer.
What is new in this research?
Old technique
• Polishing by emery paper.
• Inconsistent surface texture.
New technique
• High precision machining.
• Consistent surface texture.
14
1. Surface Preparation
What is new in this research?
2. Using surfactants to enhance the stability of
nanofluids.
• Surfactant is a compound that lowers the surface
tension.
• Sodium dodecylbenzenesulfonate (SDBS).
15
Nanofluid Preparation
• Deionized water.
• Al2O3 , Particle size =40 nm ,(0.05%wt)
• Sodium dodecylbenzenesulfonate “SDBS”
(0.1%wt).
19
1. Li et al, Evaluation on dispersion behavior of the aqueous copper nano-
suspensions.
2. Wang et al, Influence of pH and SDBS on the Stability and Thermal
Conductivity of Nanofluids.
Experimental Setup
20
q”
Boiling curves on Ra=60 nm
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0 2 4 6 8 10 12 14
q”MW/m2
ΔT
Water Before
NF,SDBS(0.1%)
23
Boiling curves on Ra=60 nm
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0 2 4 6 8 10 12 14
q”MW/m2
ΔT
Water Before
NF,SDBS(0.1%)
NF,SDBS(1.0%)
24
Boiling curves on Ra=60 nm
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0 2 4 6 8 10 12 14
q”MW/m2
ΔT
Water Before
NF,SDBS(0.1%)
NF,SDBS(1.0%)
Water After
25
Boiling curves on Ra=60 nm
• Heat transfer enhancement in natural convection
regime and deterioration in nucleate boiling
regime.
• Nanoparticles deposition has been noticed.
• ONB has been delayed using Nanofluids.
• Increasing SDBS concentration has effectively
eliminated deposition and thus heat transfer
enhancement is achieved.
• No deposition was confirmed by boiling pure
water on the same surface from the Nanofluid
experiment.
26
Water boiling curves
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0 2 4 6 8 10 12 14 16 18 20
q”MW/m2
ΔT
Ra=6 nm
Ra=60 nm
27
Boiling curves on R=6 nm
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0 2 4 6 8 10 12 14 16 18 20
q”MW/m2
ΔT
Water Before
NF,SDBS(0.1%)
NF,SDBS(0.0%)
Water After
28
Boiling curves on R=6 nm
• Heat transfer is affected by the surface
roughness.
• SDBS accelerates Onset of Nucleate
Boiling(ONB).
• Heat transfer enhancement is achieved with
and without adding SDBS.
• No deposition is noticed.
• Nanoparticle size is larger than surface
roughness.
30
Boiling at 0.2 MW/m2
Nanofluid Water
31
Boiling at 0.4 MW/m2
Nanofluid Water
32
Boiling at Critical Heat Flux
Nanofluid Water
33
Conclusions
• Modern manufacturing technologies
introduced new types of fluids.
• Nanofluid heat transfer is greatly affected by
initial surface conditions.
• Surfactants enhance stability of Nanofluids.
• Heat transfer deterioration results from
Nanoparticles deposition.
34
Future Work
• Develop a matrix to quantify the contribution
of each component used in Nanofluid
preparation.
• Test the performance of Nanofluid on very
rough surface.
• Understanding the Nanofluid interactions with
active nucleation sites using engineered Nano-
indentation.
35
Publication
• N.A. Almalki, M. Hamda, M. S. Hamed, On The Effect
of Initial Surface Condition on Pool Boiling of
Nanofluids,9th International Conference on Boiling
and Condensation Heat Transfer, April 26-30, 2015 –
Boulder, Colorado. (Extended Abstract Accepted)
36
Acknowledgement
• Alex Yip
• M. Tauhiduzzaman
Thanks for your attention.
hamdamr@mcmaster.ca

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Semianr Presentation

  • 1. Presented by: Mohamed Hamda M.A.Sc Candidate Supervisor: Dr. M. Hamed On The Effect of Initial Surface Condition on Pool Boiling of Nanofluids
  • 2. Outline • Pool Boiling. • Nanofluids. • Literature review. • Recent Research in TPL. • Current research. • Conclusion. • Future work. • Publications. 2
  • 3. Why Pool Boiling? • Free Convection - Water: 20 - 100 (W/(m2K)) • Forced Convection - Water: 50 - 10.000 (W/(m2K)) • Boiling Water : 3.000 - 100.000 (W/(m2K)) Boiling Heat transfer coefficients are the highest among different heat convection mechanisms. 6
  • 4. Pool Boiling Curve 7 * Heat and Mass Transfer: Fundamentals & Applications,Fourth Edition, Yunus A. Cengel
  • 5. Thermal conductivity of different materials Liquids Metals k - W/(m.K) Steel, Carbon 1% 43 Aluminium 205 Copper 401 k - W/(m.K) Alcohol 0.17 Engine Oil 0.15 Water 0.58 8 • The thermal conductivity of liquids is three orders of magnitude less than of metals. • The idea is to increase the thermal conductivity of liquids.
  • 6. How can we do that? • Powder of metal has particles of certain size (10 ~ 100 nm) dispersed into liquid. • This mixture is now called Nanofluid or Nanoparticles suspension. 9
  • 7. Is Nanofluid a novel idea? • Maxwell model (1881) – Effective thermal conductivity increases with the volume fraction of the solid particles as well as the ratio of the surface area to volume of the particle. – Confined to millimeter-sized particles. – Not practical (severe clogging problems). • Lee, Choi and et al. (1999) – Reported 20% increase in the thermal conductivity of CuO nanoparticles (10 nm) suspended in ethylene glycol. 10
  • 8. Literature Review 11 * O. Ahmed, M.S. Hamed, Experimental investigation of the effect of particle deposition on pool boiling of nanofluids
  • 9. Recent Research in TPL 12 Researcher (Year) Experiment Type Ra (nm) Concentration % Nanofluid Material Particle size pH Remarks Osama Ahmed (2011) Pool Boiling 100 ~ 150 50 0.01 0.1 0.5 Al2O3 40 ~ 50 nm 5 and 6.5 Enhancement & deterioration Ahmed Abd El- hady (2013) Pool and Jet Impingement Boiling 20, 80 and 420 0.005 0.01 Al2O3 CuO 10 nm 50 nm 6.5 Enhancement & deterioration
  • 10. Findings from Literature Review 13 • Contradicting results! • Heat transfer deterioration is always noticed with nanoparticles deposition on heated surface. • Most enhancement results were reported for heated wires. • Deterioration is more likely to happen with flat or horizontal heated surfaces. • Heater geometry affects Nano fluid heat transfer.
  • 11. What is new in this research? Old technique • Polishing by emery paper. • Inconsistent surface texture. New technique • High precision machining. • Consistent surface texture. 14 1. Surface Preparation
  • 12. What is new in this research? 2. Using surfactants to enhance the stability of nanofluids. • Surfactant is a compound that lowers the surface tension. • Sodium dodecylbenzenesulfonate (SDBS). 15
  • 13. Nanofluid Preparation • Deionized water. • Al2O3 , Particle size =40 nm ,(0.05%wt) • Sodium dodecylbenzenesulfonate “SDBS” (0.1%wt). 19 1. Li et al, Evaluation on dispersion behavior of the aqueous copper nano- suspensions. 2. Wang et al, Influence of pH and SDBS on the Stability and Thermal Conductivity of Nanofluids.
  • 15. Boiling curves on Ra=60 nm 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 0 2 4 6 8 10 12 14 q”MW/m2 ΔT Water Before NF,SDBS(0.1%) 23
  • 16. Boiling curves on Ra=60 nm 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 0 2 4 6 8 10 12 14 q”MW/m2 ΔT Water Before NF,SDBS(0.1%) NF,SDBS(1.0%) 24
  • 17. Boiling curves on Ra=60 nm 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 0 2 4 6 8 10 12 14 q”MW/m2 ΔT Water Before NF,SDBS(0.1%) NF,SDBS(1.0%) Water After 25
  • 18. Boiling curves on Ra=60 nm • Heat transfer enhancement in natural convection regime and deterioration in nucleate boiling regime. • Nanoparticles deposition has been noticed. • ONB has been delayed using Nanofluids. • Increasing SDBS concentration has effectively eliminated deposition and thus heat transfer enhancement is achieved. • No deposition was confirmed by boiling pure water on the same surface from the Nanofluid experiment. 26
  • 19. Water boiling curves 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 0 2 4 6 8 10 12 14 16 18 20 q”MW/m2 ΔT Ra=6 nm Ra=60 nm 27
  • 20. Boiling curves on R=6 nm 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 0 2 4 6 8 10 12 14 16 18 20 q”MW/m2 ΔT Water Before NF,SDBS(0.1%) NF,SDBS(0.0%) Water After 28
  • 21. Boiling curves on R=6 nm • Heat transfer is affected by the surface roughness. • SDBS accelerates Onset of Nucleate Boiling(ONB). • Heat transfer enhancement is achieved with and without adding SDBS. • No deposition is noticed. • Nanoparticle size is larger than surface roughness. 30
  • 22. Boiling at 0.2 MW/m2 Nanofluid Water 31
  • 23. Boiling at 0.4 MW/m2 Nanofluid Water 32
  • 24. Boiling at Critical Heat Flux Nanofluid Water 33
  • 25. Conclusions • Modern manufacturing technologies introduced new types of fluids. • Nanofluid heat transfer is greatly affected by initial surface conditions. • Surfactants enhance stability of Nanofluids. • Heat transfer deterioration results from Nanoparticles deposition. 34
  • 26. Future Work • Develop a matrix to quantify the contribution of each component used in Nanofluid preparation. • Test the performance of Nanofluid on very rough surface. • Understanding the Nanofluid interactions with active nucleation sites using engineered Nano- indentation. 35
  • 27. Publication • N.A. Almalki, M. Hamda, M. S. Hamed, On The Effect of Initial Surface Condition on Pool Boiling of Nanofluids,9th International Conference on Boiling and Condensation Heat Transfer, April 26-30, 2015 – Boulder, Colorado. (Extended Abstract Accepted) 36
  • 29. Thanks for your attention. hamdamr@mcmaster.ca